Apparatus and methods for impinging fluids on substrates

ABSTRACT

Herein are disclosed apparatus and methods for impinging fluids, e.g. heated fluids, onto the surface of substrates and then locally removing the impinged fluid. The apparatus may comprise at least first and second fluid delivery outlets that are in diverging relation to each other. The apparatus may comprise at least first and second fluid capture inlets that are locally positioned relative to the first and second fluid delivery outlets, respectively. The apparatus and method may be used e.g. to impinge fluids onto two converging substrates and may be used to heat the surfaces of the substrates so as to facilitate melt-bonding the substrates to each other.

CROSS REFERENCE TO RELATED APPLICATION

This application claims the benefit of U.S. Provisional PatentApplication No. 61/288959, filed Dec. 22, 2009, the disclosure of whichis incorporated by reference herein in its entirety.

BACKGROUND

Fluids, e.g. heated fluids, are often impinged upon a substrate for avariety of purposes. For example, heated fluids may be impinged upon asubstrate for purposes of annealing, drying of a surface coating,promoting a chemical reaction or a physical change, and the like. Often,the impinged fluid is allowed to escape into the surrounding atmosphere,where it may be allowed to disperse or may be at least partially removedby a duct, hood, or the like.

SUMMARY

Herein are disclosed apparatus and methods for impinging fluids, e.g.heated fluids, onto the surface of substrates and then locally removingthe impinged fluid. The apparatus may comprise at least first and secondfluid delivery outlets that are in diverging relation to each other. Theapparatus may comprise at least first and second fluid capture inletsthat are locally positioned relative to the first and second fluiddelivery outlets, respectively. The apparatus and method may be usede.g. to impinge fluids onto two converging substrates and may be used toheat the surfaces of the substrates so as to facilitate melt-bonding thesubstrates to each other.

In one aspect, disclosed herein is an apparatus for impinging fluid ontoat least a first surface of a first moving substrate and a first surfaceof a second moving substrate and locally removing the impinged fluid,comprising: at least one first fluid delivery outlet; at least one firstfluid capture inlet that is locally positioned relative to the firstfluid delivery outlet; at least one second fluid delivery outlet; atleast one second fluid capture inlet that is locally positioned relativeto the second fluid delivery outlet; and wherein the at least one firstfluid delivery outlet and the at least one second fluid delivery outletare in diverging relation.

In another aspect, disclosed herein is a method of impinging heatedfluid onto, and locally removing the impinged fluid from, a firstsurface of a first moving substrate and a first surface of a secondmoving substrate, the method comprising: providing at least one firstfluid delivery outlet and at least one first fluid capture inlet that islocally positioned relative to the first fluid delivery outlet;providing at least one second fluid delivery outlet and at least onesecond fluid capture inlet that is locally positioned relative to thesecond fluid delivery outlet; passing the first moving substrate by thefirst fluid delivery outlet and impinging heated fluid from the firstoutlet onto the first major surface of the first moving substrate;passing the second moving substrate by the second fluid delivery outletand impinging heated fluid from the second outlet onto the first majorsurface of the second moving substrate; and, locally capturing at least60% of the total volumetric flow of impinged fluid by way of the fluidcapture inlets and removing the locally captured fluid through fluidremoval channels that are fluidly connected to the fluid capture inlets;and wherein the first and second moving substrates are convergingsubstrates.

BRIEF DESCRIPTION OF THE DRAWINGS

FIG. 1 is a side view of an exemplary laminate comprising an exemplaryfibrous web that is surface-bonded to an exemplary substrate with aloft-retaining bond.

FIG. 2 is an illustrative depiction, in side schematic view in partialcross section, of a portion of a laminate comprising a fibrous web withfiber portions surface-bonded to a substrate.

FIG. 3 is an illustrative depiction, in side schematic view in partialcross section, of a portion of a laminate comprising a fibrous web witha fiber portion embedded in a substrate.

FIG. 4 is an illustrative depiction, in side schematic view in partialcross section of a laminate comprising a fibrous web with a fiberportion fused to a substrate.

FIG. 5 is a scanning electron micrograph taken at 130× magnification, ofan exemplary laminate comprising a nonwoven fibrous web surface-bondedto a substrate.

FIG. 6 is a scanning electron micrograph taken at 180× magnification, ofan exemplary laminate comprising a nonwoven fibrous web surface-bondedto a substrate.

FIG. 7 is a top view of two exemplary substrates bonded to an exemplaryfibrous web.

FIG. 8 is a side view of an exemplary apparatus and process that may beused to bond a first substrate to a second substrate.

FIG. 9 is an expanded side view in partial cutaway of a portion of theexemplary apparatus and process of FIG. 8.

FIG. 10 a is a cross sectional diagrammatic illustration of a portion ofan exemplary apparatus and process that may be used to impinge heatedfluid onto a substrate and to locally remove the impinged fluid.

FIGS. 10 b and 10 c depict additional ways in which the exemplaryapparatus and process of FIG. 10 a may be operated.

FIG. 11 is a side view in partial cutaway of an exemplary apparatus andprocess that may be used impinge heated fluid onto two substrates and tolocally remove the impinged fluid, and to bond the two substratestogether.

FIG. 12 is a cross sectional diagrammatic illustration of a portion ofanother exemplary apparatus and process that may be used to impingeheated fluid onto a substrate and to locally remove the impinged fluid.

Like reference numbers in the various figures indicate like elements.Some elements may be present in similar or identical multiples; in suchcases the elements may comprise the same reference number, with one ormore of the elements designated by a prime (′) for convenience ofdescription. Unless otherwise indicated, all figures and drawings inthis document are not to scale and are chosen for the purpose ofillustrating different embodiments of the invention. In particular thedimensions of the various components are depicted in illustrative termsonly, and no relationship between the dimensions of the variouscomponents should be inferred from the drawings, unless so indicated.Although terms such as “top”, bottom”, “upper”, lower”, “under”, “over”,“front”, “back”, “outward”, “inward”, “up” and “down”, and “first” and“second” may be used in this disclosure, it should be understood thatthose terms are used in their relative sense only unless otherwisenoted.

DETAILED DESCRIPTION

Shown in FIG. 1 is a side perspective view of an exemplary laminate 150comprising fibrous web 110 that is bonded to substrate 120. Fibrous web110 is comprised of fibers 111, and comprises first major surface 112and second, oppositely-facing major surface 113. (Those of ordinaryskill in the art will recognize that surfaces 112 and 113 of web 110 maynot be perfectly planar and/or continuous physical surfaces since theyare collectively defined by outwardmost portions of certain fibers 111of web 110). Laminate 150 further comprises substrate 120, whichcomprises first major surface 121 and second, oppositely-facing majorsurface 122. Substrate 120 may optionally comprise protrusions 123 thatprotrude from major surface 122.

In the illustrated embodiment, fibrous web 110 is surface-bonded tosubstrate 120 (specifically, first major surface 112 of fibrous web 110is surface-bonded to first major surface 121 of substrate 120). By thisis meant that fibrous web 110 is attached to substrate 120 by way ofsome fibers 111 of surface 112 of web 110 being surface-bonded to firstmajor surface 121 of substrate 120. As shown in an illustrative mannerin FIG. 2, the designation that fibers 111 are surface-bonded to firstmajor surface 121 of substrate 120 means that parts of fiber surfaces115 of fiber portions 114 of fibers 111 are melt-bonded to first majorsurface 121 of substrate 120, in such a manner as to substantiallypreserve the original (pre-bonded) shape of first major surface 121 ofsubstrate 120, and to substantially preserve at least some portions offirst major surface 121 of substrate 120 in an exposed condition, in thesurface-bonded area.

The requirement that surface bonding substantially preserves theoriginal shape of first major surface 121 means that surface-bondedfibers may be distinguished from fibers that are bonded to a substratein a manner that results in fiber portions being embedded (e.g.,partially or completely encapsulated) within the substrate (as shown inan illustrative manner in FIG. 3) by way of at least partial penetrationof the fibers into the substrate, deformation of the substrate, and thelike. Quantitatively, surface-bonded fibers may be distinguished fromembedded fibers 116 by way of at least about 65% of the surface area ofthe surface-bonded fiber being visible above the surface of thesubstrate in the bonded portion of the fiber (although inspection frommore than one angle may be necessary to visualize the entirety of thesurface area of the fiber). The substantial preservation of the original(pre-bonded) shape of substrate 120 may also be manifested by theabsence of any gross change in the physical shape of first major surface121 (e.g. wrinkling, buckling, penetration of portions of substrate 120into the interstitial spaces of web 110, etc.).

The requirement that surface bonding substantially preserves at leastsome portions of first major surface 121 in an exposed condition meansthat surface-bonded fibers may be distinguished from fibers that arebonded to a substrate in a manner that results in the fibers beingsufficiently melted, densified, compacted, commingled etc., so as toform a continuous bond. By continuous bond is meant that fibersimmediately adjacent to first major surface 121 of substrate 120 havecommingled and/or densified sufficiently (e.g., melted together so as topartially or completely lose their identity as individual fibers) toform a continuous layer of material atop, and in contact with, firstmajor surface 121. (Those of ordinary skill in the art will recognizethe possibility of occasional voids and the like in a “continuous”layer, and will appreciate that in this context the term continuous canbe interpreted to mean that, in a bonded area, the continuous,densified-fiber layer is atop, and in contact with, at least about 95%of the area of first major surface 121 of substrate 120). Thus,surface-bonded fibers can be distinguished from fibers bonded in acontinuous bond, by the presence of numerous exposed areas in whichfirst major surface 121 of substrate 120 is visible between thesurface-bonded fibers that make up first major surface 112 of fibrousweb 110.

Scanning electron micrographs (at 130× and 180× magnification,respectively) of exemplary nonwoven fibrous webs surface-bonded tosubstrates are shown in FIGS. 5 and 6. In these micrographs, theabove-described surface bonding of fiber portions to the surface of thesubstrate is readily apparent, with minimal deformation or damage to thebonded fiber portions or to the substrate, and with numerous exposedareas of the surface of the substrate being visible amongst thesurface-bonded fibers.

As defined herein, the term surface-bonded means that a web ismelt-bonded to a substrate primarily by the above-describedsurface-bonded fiber portions, and furthermore means that in the absenceof such surface bonds the fibrous web and the substrate would not remainbonded together. Those of ordinary skill in the art will recognize thatthe term surface-bonded as used in this manner does not encompasssituations in which the primary bonding between a fibrous web and asubstrate is by some other melt-bonding mechanism (e.g., by embedding offibers into the substrate, and the like), with surface-bonded fiberportions only being found occasionally within the bonded area or areasof the web. Those of ordinary skill in the art will thus appreciate thatsurface-bonding as described herein does not encompass such melt-bondingas is commonly achieved e.g. by ultrasonic bonding, by compressionbonding (e.g., as achieved by passing substrates through a heated nip atrelatively high pressure), by extrusion-lamination and the like. Suchprocesses are well-known to result in large-scale deformation and/orphysical changes of the fiber portions and/or the substrate, in theformation of the bond. Those of ordinary skill in the art will furtherappreciate that fibrous webs that are bonded to substrates that arestill in a molten, semi-molten, soft, etc. state, (such as extrudedmaterials that have not yet cooled e.g. to a solid condition), may notcomprise surface bonding, since bonding to a substrate that is still atsuch a high temperature and/or is still considerably deformable, maycause the fibers to become embedded, may cause the formation of acontinuous bond, or both.

Those of skill in the art will further recognize that while embeddedfiber portions, small-scale quasi-continuously bonded regions, and thelike, may occasionally occur in a web that has been surface-bonded to asubstrate as described herein, such features may represent only theinherent sporadic occurrence of such features in the bonding process. Asstated above, the term surface-bonded means that while such embeddedfiber portions and/or quasi-continuously bonded fiber regions may bepresent to a small extent, the majority of the bonds between fiberportions and the substrate are surface bonds, such that in the absenceof such surface bonds, any adventitious bonding by way of embeddedfibers and/or quasi-continuously bonded regions would be so weak thatthe fibrous web and the substrate would not remain bonded together.

Those of ordinary skill in the art will still further recognize thatwhile surface-bonding of fiber portions to a substrate as describedherein may lead to individual bonds that are weaker than bonds obtainedby embedding fibers within the substrate or continuously bonding fibersto the substrate, surface-bonding as described herein may neverthelessprovide an acceptable bond between a fibrous web and a substrate ifperformed over a sufficiently large area or areas. That is,surface-bonding may be advantageously performed over a large area orareas (herein termed “area-bonding”), as opposed to the small-areabonding (often called point-bonding) that is often achieved byultrasonic bonding and the like. Such area-bonding means that the largenumber of surface-bonded fiber portions (that may be randomly and/oruniformly present over the bonded area) can collectively provideadequate bond strength for laminate 150 to be handled and to performsatisfactorily in various end uses. In various embodiments, such surfacebonded areas between fibrous web 110 and substrate 120 may each comprisean area of at least about 100 square mm, at least about 400 square mm,or at least 1000 square mm. One of ordinary skill in the art will thusagain be able to readily distinguish such area-bonding from the local orpoint bonding that is often employed in other melt-bonding processes.

At least by the methods disclosed herein, surface-bonding can be easilyperformed over a large proportion of the area of overlap or contactbetween a fibrous web and a substrate. Specifically, fibrous web 110 andsubstrate 120 may comprise an overlapped area (e.g., in which firstsurface 112 of web 110, and first surface 121 of substrate 120, arefacing each other and/or are in contact with each other). Of thisoverlapped area, at least about 70%, at least about 80%, at least about90%, or substantially all, may comprise surface-bonded area or areas.

Surface-bonding as disclosed herein may provide advantages over othermelt-bonding methods. Specifically, within the bonded area,surface-bonding may minimize any deformation of substrate 120 and mayminimize the number of fibers 111 that are embedded within substrate 120and/or are continuously bonded to substrate 120. Thus, laminate 150 mayremain quite flexible even in the bonded area.

Surface-bonding as disclosed herein may be performed to the point thatsubstrate 120 and fibrous web 110 are not separable from each other, atall or without severely damaging one or both of substrate 120 andfibrous web 110.

In some embodiments, surface-bonded fibers may generally, orsubstantially, retain their original (pre-bonded) shape. In suchembodiments, shape-retaining surface-bonded fibers may be distinguishedfrom fibers that are bonded to a substrate by way of a fiber portionbeing fused to the substrate, (with the term fused meaning that in thebonding process the fiber portion has become substantially deformed fromits original pre-bonded physical structure and shape, e.g. the fiberportion has become substantially flattened), as shown in an illustrativemanner in FIG. 4. Quantitatively, shape-retaining surface-bonded fibersmay be distinguished from fused fibers 117 by way of the surface-bondedfibers remaining sufficiently circular in cross section as to exhibit anaspect ratio (i.e., ratio of the largest cross sectional dimension ofthe fiber to the smallest cross sectional dimension) in the bondedportion of the fiber of no more than about 2.5:1 (as obtained by anaverage based on a number of representative fibers). In variousembodiments, the fibers may comprise an aspect ratio of no more thanabout 2:1, or no more than about 1.5:1. Those of ordinary skill in theart will realize that this method of identification of shape-retainingsurface-bonded fibers may only be appropriate for fibers of generallycircular cross sectional shapes as originally made; if fibers of othershapes are used, it may be necessary to compare the cross sectionalshape of the fibers as originally made to the shape after a bondingoperation, in order to make the determination. Also, those of ordinaryskill in the art will recognize that some deformation of the crosssectional shape of some portion of some shape-retaining surface-bondedfibers may occasionally occur due to the presence of other fibers incontact with portions of the fiber while the fibers are at a hightemperature (some such occurrences are visible in FIG. 6).Shape-retaining surface-bonded fibers that exhibit deformation for thisreason should not be equated with fused fibers.

In the illustrated embodiment of FIG. 1, fibrous web 110 is bonded tosubstrate 120 by way of a loft-retaining bond. By this is meant thatfibrous web 110 is melt-bonded to substrate 120 such that fibrous web110 retains a significant amount of the loft exhibited by fibrous web110 prior to the bonding process. Loft is a term of art with regard tofibrous webs, and is a measure of the degree of openness, lack ofcompaction, presence of interstitial spaces, etc., within a fibrous web.As such, any common measure of loft may be used. For convenience, hereinthe loft of a fibrous web will be represented by the ratio of the totalvolume occupied by the web (including fibers as well as interstitialspaces of the web that are not occupied by fibers) to the volumeoccupied by the material of the fibers alone. Using this measure, aloft-retaining bond as described herein is defined as one in whichbonded fibrous web 110 comprises a loft that is at least 80% of the loftexhibited by the web prior to, or in the absence of, the bondingprocess. If only a portion of fibrous web 110 has substrate 120 bondedthereto, the retained loft can be easily ascertained by comparing theloft of the web in the bonded area to that of the web in an unbondedarea. If the entirety of fibrous web 110 has substrate 120 bondedthereto (or if the web in an unbonded area has also undergone compactionduring the bonding process), it may be necessary to compare the loft ofthe bonded web to that of a sample of the same web prior to beingbonded. In various embodiments, laminate 150 comprises a loft-retainingbond such that fibrous web 110 comprises at least 90%, at least 95%, orsubstantially all, of its prebonded loft.

Those of ordinary skill in the art will recognize that in someembodiments laminate 150 may not comprise a surface-bonded laminate asdescribed herein (e.g., a significant number of fibers 111 comprisingfirst major surface 112 of fibrous web 110 may be embedded withinsubstrate 120 and/or continuously bonded to substrate 120), but in suchcases fibrous web 110 may nevertheless be bonded to substrate 120 in aloft-retaining bond.

Loft-retaining bonding as disclosed herein may provide advantages overother melt-bonding methods. Specifically, within the bonded area,loft-retaining bonding may leave the fibers of fibrous web 110 that arenot on first major surface 112 of web 110 intact and/or not melt-bondedto substrate 120. Thus, fibrous web 110 may remain lofty, resilientand/or flexible even in the bonded area (in such cases, fibrous web 110may be more easily engageable by male fastening elements, may present amore pleasing tactile feel and/or appearance, etc). In contrast, otherbonding methods may disadvantageously crush or densify most or all ofthe fibers in the bonded area and/or may melt-bond them to thesubstrate, with loss of desirable properties such as loft andflexibility. Those of ordinary skill in the art will thus appreciatethat loft-retained bonding as described herein does not encompass suchmelt-bonding as is commonly achieved e.g. by ultrasonic bonding, bycompression bonding (e.g., as achieved by passing substrates through aheated nip at relatively high pressure), by extrusion-lamination and thelike, when such processes result in significant crushing and/ordensification of the bonded web.

Those of ordinary skill in the art will recognize that other bondingmethods, e.g. supplemental point bonding, may be used in certainlocations of the laminate in addition to the herein-described surfacebonding and/or loft-retained bonding, e.g., if desired to enhance theoverall bonding.

While methods presented herein (e.g., impingement of heated fluid uponthe surfaces of two converging substrates; or, impingement of heatedfluid upon the surfaces of two converging substrates with local removalof the impinged heated fluid) may be particularly suitable for theproduction of surface-bonded laminates, loft-retained bonded laminates,or both, those of ordinary skill in the art will appreciate, based onthe disclosures herein, that other methods may also be suitable. Suchmethods may include any process by which heat can be imparted to thefirst surfaces of two substrates such that the first surfaces of the twosubstrates may be melt-bonded together to achieve the structuresdescribed herein.

Substrate 120 may be any substrate to which it is desired tosurface-bond fibrous web 110. Substrate 120 may be made of any suitablethermoplastic polymeric material (e.g., a material that ismelt-bondable). Such materials may include e.g. polyolefins, polyesters,polyamides, and various other materials. Examples of suitablepolyolefins include polyethylene, polypropylene, polybutylene, ethylenecopolymers, propylene copolymers, butylene copolymers, and copolymersand blends of these materials. The substrate may comprise variousadditives and the like, as are well known in the art, as long as suchadditives do not unacceptably reduce the ability of the substrate to bemelt bonded. Substrate 120 may be multilayer, e.g. a coextrudedmultilayer film, as long as first major surface 121 is able to bemelt-bonded to at least some of the fibers of fibrous web 110.

In some embodiments, substrate 120 may comprise a preformed substrate,by which is meant that substrate 120 is a pre-existing, previously-madefilm whose physical properties have generally fully developed. Thisshould be contrasted e.g. with a case in which a substrate is made(e.g., extruded) and taken generally directly into the herein-describedbonding process in a condition in which it is still generally molten,semi-molten, soft, or the like.

Substrate 120 may be any desired thickness. In various embodiments, thethickness of substrate 120 (not including the height of the protrusions)may be less than about 400 microns, less than about 200 microns, lessthan about 100 microns, or less than about 50 microns. In someembodiments, substrate 120 does not comprise any adhesive (i.e., hotmelt adhesive, pressure sensitive adhesive, and the like) e.g. in theform of coatings on a major surface of the web.

In some embodiments, substrate 120 may be continuous, i.e. without anythrough-penetrating holes. In other embodiments, substrate 120 may bediscontinuous, e.g. comprising through-penetrating perforations and thelike. In some embodiments, substrate 120 may be comprised of a dense,nonporous material. In some embodiments, substrate 120 may be comprisedof a porous material. In particular embodiments, substrate 120 maycomprise a fibrous web, e.g. a nonwoven fibrous web.

In some embodiments, first major surface 121 and second,oppositely-facing major surface 122 of substrate 120 may be free ofprotrusions. In other embodiments, optional protrusions 123 may protrudefrom second major surface 122 of substrate 120, as shown in theexemplary design of FIG. 1. (In this particular design, protrusions 123are on the opposite side of substrate 120 from the side that is to bebonded). Protrusions 123 can be of any desired type, shape or design,present at any desired density per area of substrate 120, as desired forany suitable purpose. Protrusions 123 may be integral with (that is, ofthe same composition, and formed at the same time with as a unit)substrate 120.

In various embodiments, protrusions 123 may comprise a maximum height(above surface 122) of at most about 3 mm, about 1.5 mm, about 0.8 mm,or about 0.4 mm. In additional embodiments, protrusions 123 may comprisea minimum height of at least about 0.05 mm, about 0.1 mm, or about 0.2mm. In various embodiments, protrusions 123 may comprise an aspect ratio(the ratio of the protrusion height to the protrusion largest width) ofat least about 2:1, at least about 3:1, or at least about 4:1.

In some embodiments, protrusions 123 comprise male fastening elements,e.g. hooks, of the type that are capable of engaging with a fibrousmaterial and which can serve as the hook component of a so-called hookand loop fastening system. Any such male fastening elements can be used.In particular embodiments, fastening elements may be used that eachcomprise a stem and a relatively large head (that may be e.g. generallymushroom-shaped, a flattened disc, and the like), of the general typedescribed in U.S. Pat. Nos. 6,558,602, 5,077,870, and 4,894,060.Suitable substrates with protrusions comprising male fastening elementsinclude e.g. those products available from 3M Company, St. Paul, Minn.,under the trade designation CS200 and CS 600. Other suitable substratesinclude e.g. those described in U.S. Pat. Nos. 7,067,185 and 7,048,984.

Bonding as described herein may be particularly advantageous in themelt-bonding of fibrous web 110 to a substrate 120 that comprisesprotrusions 123 (in particular, male fastening elements), because thebonding may be able to be performed without significantly damaging (e.g.deforming, crushing, flattening, etc.) the protrusions in the bondedarea. Thus, in some embodiments, bonding processes as described hereinare performed such that substrate 120 of laminate 150 comprisesprotrusions 123 that have not been significantly damaged. By notsignificantly damaged means that upon visual inspection (e.g., by meansof a microscope sufficiently powerful to reveal details of individualprotrusions), no more than one protrusion in every ten protrusionsdisplays any damage such as deformation, crushing, melting, and thelike, when compared to protrusions that have not undergone the bondingprocess. In further embodiments, fewer than one protrusion in twentydisplays damage. In an additional embodiment, substantially all of theprotrusions are free of damage. For the particular case in which theprotrusions of the substrate are male fastening elements, the absence ofsignificant damage to the protrusions may also be manifested in theretained peel performance of the substrate. For example, when mated withany suitable loop component and subjected to any of the peel testswell-known for quantitatively characterizing the performance ofcomponents of hook-and-loop fastening systems, the substrate, afterbeing subjected to the bonding processes described herein, may retain atleast at about 80 percent of the peel performance of the substrate asoriginally made. In various embodiments, the peel performance of thesubstrate may remain at least at about 90%, or at least at about 95%, ofthe peel performance of the substrate as originally made. Those of skillin the art will appreciate that many bonding processes significantly oreven completely crush all protrusions in the process of achieving a bondand thus will again appreciate the fundamental differences between thebonding methods and bonded laminates disclosed herein, and those in theart.

Fibrous web 110 may be any suitable fibrous web with sufficientmechanical strength to be handled as a self-supporting web and to besubjected to the bonding processes described herein. As such, it will beunderstood that laminate 150 as described herein does not encompass anyarticle that does not comprise a pre-existing, self-supporting fibrousweb that is laminated to a substrate (such non-encompassed articlesmight include e.g. meltblown fibers deposited onto a scrim, and thelike).

In some embodiments, fibrous web 110 may comprise interlaced fibers suchas achieved by weaving, knitting, stitching and the like. As such,fibrous web 110 may be comprised of a suitable fabric or textile, aslong as the materials comprising the fibers are suitable for theherein-described bonding. Thus, although web 110 may be referred tooccasionally herein for convenience of illustration as a nonwovenfibrous web, it is understood that web 110 may comprise any suitablefibrous material.

In some embodiments, fibrous web 110 comprises a nonwoven fibrous web.Any suitable self-supporting nonwoven fibrous web 110 may be used, madeof any material as desired, as long as the herein-described bonding canbe performed. Nonwoven fibrous web 110 may be e.g. a carded web,spunbonded web, a spunlaced web, an airlaid web, or a meltblown web(i.e., as long as such a web has undergone sufficient processing as torender it self-supporting). Nonwoven fibrous web 110 may be a multilayermaterial with, for example, at least one layer of a meltblown web and atleast one layer of a spunbonded web, or any other suitable combinationof nonwoven webs. For instance, nonwoven fibrous web 110 may be aspunbond-meltbond-spunbond, spunbond-spunbond, orspunbond-spunbond-spunbond multilayer material. Or, the web may be acomposite web comprising a nonwoven layer and a dense film layer, asexemplified by webs comprising nonwoven fibers bonded in arcuatelyprotruding loops to a dense film backing and available from 3M Company,St. Paul, Minn., under the trade designation Extrusion Bonded Loop.

Fibrous web 110 may be made of any suitable thermoplastic polymericmaterial (e.g., a material that is melt-bondable). Such materials mayinclude e.g. polyolefins, polyesters, polyamides, and various othermaterials. Examples of suitable polyolefins include polyethylene,polypropylene, polybutylene, ethylene copolymers, propylene copolymers,butylene copolymers, and copolymers and blends of these materials. Thoseof ordinary skill in the art will appreciate that the composition offibrous web 110 may advantageously be chosen so as to enhance themelt-bonding to substrate 120. For example, at least major surface 121of the substrate, and at least some of the fibers of the fibrous web,may be comprised substantially of e.g. polypropylene.

Fibrous web 110 may have any suitable basis weight, as desired for aparticular application. Suitable basis weights may range e.g. from atleast about 20, 30 or 40 grams per square meter, up to at most about400, 100 or 100 grams per square meter. Fibrous web 110 may comprise anysuitable loft, as previously described herein. Fibrous web 110 maycomprise any suitable thickness. In various embodiments, fibrous web 110may be at most about 5 mm, about 2 mm, or about 1 mm, in thickness. Infurther embodiments, fibrous web 110 may be at least about 0.1, about0.2, or about 0.5 mm in thickness.

In some embodiments, some or all of fibers 111 of fibrous web 110 maycomprise monocomponent fibers. In some embodiments, fibrous web 110 mayalso or instead comprise bicomponent fibers, e.g., that comprise asheath of lower-melting material surrounding a core of higher meltingmaterial. If desired, the sheath material may be chosen so as to enhanceits ability to melt-bond to substrate 120. Other fibers (e.g., staplefibers and the like) may be present. In some embodiments, fibrous web110 does not comprise any adhesive (i.e., hot melt adhesive, pressuresensitive adhesive, and the like) as might be present in the form ofadhesive particles, binder or the like, distributed throughout the webor on a major surface of the web. In some embodiments, fibrous web 110comprises certain fibers with a composition advantageously suitable forthe herein-described surface bonding, and other fibers with acomposition different from that of the surface-bonding fibers.

In certain embodiments, fibrous web 110 comprises an extended portionthat is not in overlapping relation with substrate 120. (By the methodsdisclosed herein, the exposed surface of the extended portion of fibrousweb 110 can remain generally unaffected by heat exposure during thebonding process; that is, the exposed surface is not charred or renderedglassy or any like condition indicative of unacceptably high exposure toheat). Such an extended portion of fibrous web 110 can be used e.g. asan attachment area by which laminate 150 may be attached to an item. Onesuch configuration is shown in exemplary manner in FIG. 7, in which atleast one substrate 120 is present as a narrow strip upon a wider widthof fibrous web 110. An individual piece 160 of laminate 150 can beremoved by cutting along the phantom line shown, with individual piece160 comprising extended portion 161 that can be used to attach piece 160to an item. In the particular embodiment shown in FIG. 7, an additionalextended portion 162 of fibrous web 110 is provided that extends in theopposite direction from extended portion 161, and may serve e.g. as afingerlift in the event that piece 160 is used as a hook-bearingcomponent of a hook and loop fastening system (i.e. as a hook-bearingtab). As may be useful in such an application, the exemplary substrateof FIG. 7 comprises protrusions 123 (that may be male fasteningelements, for example) that protrude from second major surface 122 ofsubstrate 120.

In the particular embodiment illustrated in FIG. 7, substrate 120 ispresent as two strips upon a wider width of fibrous web 110, with alaterally extended portion of fibrous web 110 outwardly bordering eachstrip of substrate 120 and with an additional extended portion offibrous web 110 laterally in between the strips of substrate. From thislaminate, individual pieces 160 can be cut, each piece with anattachment portion 161 and a fingerlift portion 162, e.g. for attachmentto items such as hygiene articles (e.g., diapers, personal careproducts, and the like). The attachment of portion 161 to an item may beaccomplished by any method known in the art, e.g. ultrasonic bonding,adhesive attachment, etc.

In brief, the bonding processes described herein involve the impingingof heated fluid (i.e., gaseous fluid) onto a first major surface of afirst moving substrate and the impinging of heated fluid onto a firstmajor surface of a second moving substrate. In some embodiments, themoving substrates may be converging substrates, meaning that thesubstrates are moving in a converging path in which the first majorsurface of the first substrate comes into contact with the first majorsurface of the second substrate. As disclosed herein, the impinging ofheated fluid onto the first surface of a moving substrate can raise thetemperature of the first surface of the substrate sufficiently forbonding to be achieved, without necessarily raising the temperature ofthe remaining portions of the substrate (e.g., the interior of thesubstrate and/or the second, opposing major surface of the substrate) toa point sufficient to cause unacceptable physical changes or damage. Inthe specific instance of bonding a fibrous web to a substrate, in someembodiments the temperature of the fluid-impinged surfaces of thefibrous web and of the substrate can be sufficiently raised to achievethe above-described surface-bonding, e.g. without causing the fibers tobecome embedded in the substrate, and/or without causing such melting,densification and/or solidification of the fibers immediately adjacentthe substrate surface as to cause the formation of a continuous bond.

Those of ordinary skill in the art will recognize the herein-describedbonding to be melt-bonding, i.e. in which molecules of the fiber surfacematerial and of the substrate surface material intermix while in aheated state achieved by the heated fluid impingement and then remainintermixed upon cooling and solidification. Those of ordinary skill inthe art will also appreciate that the heated fluid-impingement methodsdisclosed herein are not limited to the formation of surface-bondedlaminates as described herein, and may be used for additional purposes,e.g. for achieving melt-bonding that does not fall within the definitionof surface bonding as used herein, and even for purposes other thanmelt-bonding.

In some embodiments, the impinging of heated fluid onto a first majorsurface of a first moving substrate and the impinging of heated fluidonto a first major surface of a second moving substrate are performedsimultaneously, with the impinging of heated fluid continuingsubstantially up until the time that the first major surfaces of thesubstrate are brought into contact with each other.

Shown in FIG. 8 is an exemplary apparatus 1 that can be used at least toachieve the above-described surface bonding. In such embodiments, firstsubstrate 110 (e.g., a fibrous web) and second substrate 120 (e.g., asubstrate optionally containing protrusions) are each in contact with arespective backing surface during the impinging of heated fluid onto thefirst major surface of each substrate. Such a backing surface may serveto support the substrate, and may also be cooled to a certain amount(e.g. 100, 200, or 300 or more degrees C. below the temperature of theimpinging heated fluid), so as to assist in keeping the rest of thesubstrate sufficiently cool to prevent or minimize damage, melting,etc., of the substrate, during the time that the first major surface ofthe substrate is heated so as to facilitate the surface bonding. If asubstrate is discontinuous or porous (e.g., if the substrate is afibrous web) such a backing surface may also serve to occlude the secondmajor surface of the substrate such that the impinging fluid does notpenetrate through the thickness of the substrate and exit through thesecond major surface. Thus in these embodiments, the heating of a majorsurface of a substrate by the impinging of heated fluid as describedherein, does not encompass methods in which heated fluid is impingedupon a major surface of a substrate and passed through the substrate soas to exit through the oppositely-facing major surface.

The backing surface may in some embodiments be provided by a backingroll. Thus, in the exemplary illustration of FIG. 8, second majorsurface 113 of substrate 110 is in contact with surface 231 of backingroll 230 during the impinging of heated fluid onto first major surface112 of substrate 110. Likewise, second major surface 122 of substrate120 (or the outermost surface of protrusions 123, if such protrusionsare present), is in contact with surface 221 of backing roll 220 duringthe impinging of heated fluid onto first major surface 121 of substrate120.

In some embodiments, a preheat roll can be used to preheat a surface ofone or both of substrates 110 and 120 prior to the impinging of theheated fluid. In the exemplary illustration of FIG. 8, major surface 121of substrate 110 is brought into contact with surface 211 of preheatroll 210 prior to the impinging of heated fluid onto major surface 121of substrate 110.

In the illustrated embodiment of FIG. 8, backing roll 220 and backingroll 230 combine to form lamination nip 222 in which first major surface112 of substrate 110 and first major surface 121 of substrate 120 arebrought into contact with each other while at a temperature (establishedby the heated fluid impingement) sufficient to cause at leastsurface-bonding of substrates 110 and 120 to each other. As mentionedpreviously herein, it may be advantageous to perform such bonding underconditions which minimize any damage, crushing and the like, to anycomponent of substrates 110 and 120. This may be particularly useful inthe event that, as shown in FIG. 8, substrate 120 comprises protrusions(e.g., that might be susceptible to being deformed or crushed). Thus,backing rolls 230 and 220 may be arranged so as to operate nip 222 atvery low pressure in comparison to the pressures normally used in thelamination of materials (for which relatively high pressure is oftenpreferred). In various embodiments, the bonding of substrates 110 and120 together may be performed with a lamination nip pressure of lessthan about 15 pounds per linear inch (27 Newtons per linear cm), lessthan about 10 pli (18 Nlc), or less than about 5 pli (9 Nlc). In furtherembodiments, backing roll 230, backing roll 220, or both, may compriseat least a surface layer of a relatively soft material (e.g., a rubbermaterial with a hardness of less than 70 on the Shore A scale). Such arelatively soft surface layer may be achieved e.g. by the use of a rollwith a permanently attached soft surface coating, by the use of aremovable sleeve of soft material, by covering the surface of thebacking roll with relatively soft and resilient tape, and the like. Ifdesired, the surface of one or both backing rolls may be stepped acrossthe face of the roll so a to provide lamination pressure selectively incertain locations.

Upon exiting lamination nip 222, laminate 150 (which in some embodimentsmay be surface-bonded, loft-retaining bonded, or both) may be cooled ifdesired, e.g. by contacting one or both major surfaces of laminate 150with a cooling roll, by the impinging of a cooling fluid upon one orboth surfaces of laminate 150, and the like. Laminate 150 may thereafterbe processed through any suitable web-handling process, rolled up,stored, etc. For example, additional layers may be coated or laminatedon laminate 150, individual pieces may be cut therefrom as describedpreviously, and so on.

As mentioned, bonding apparatus and methods described herein may beparticularly advantageous for the bonding of substrates comprisingeasily crushed protrusions. In addition, bonding apparatus and methodsdescribed herein may be particularly suited for the bonding of porousmaterials such as fibrous webs. Such webs may comprise a self-insulatingcapacity such that the first major surface of the fibrous web may beheated by the impinging of heated fluid, while the remainder (interiorand second major surface) of the web remain relatively cool. (Someadventitious additional fiber-fiber bonding may occur within the fibrousweb during the heat exposure). Bonding processes as described herein mayalso be especially suitable for the bonding of fibrous webs to asubstrate while retaining the loft of the fibrous web, as mentionedpreviously.

Those of ordinary skill in the art will appreciate that the heating ofmultiple substrates, e.g. converging substrates, by impinging heatedfluid onto a first major surface of a first moving substrate and theimpinging of heated fluid onto a first major surface of a second movingsubstrate (in particular as achieved by use of the nozzles describedlater herein), may be suitable for many uses, including uses other thanthe aforementioned bonding or surface-bonding. For example, such methodsmay be used to evaporate liquids from substrates, to modify the surfacestructure of substrates by annealing or the like, to promote a chemicalreaction or surface modification, to dry, harden, and/or crosslink acoating present on the surface, and so on.

The impinging of heated fluid onto first major surface 112 of substrate110, and the impinging of heated fluid onto first major surface 121 ofsubstrate 120, may be achieved by the use of nozzle 400. A nozzle 400 ofthe exemplary type shown in FIG. 8 is shown in greater detail in FIG. 9.As shown in side view in FIG. 9 (viewed along an axis transverse to thedirection of motion of substrates 110 and 120, i.e., an axis alignedwith the long axes of backing rolls 220 and 230), nozzle 400 comprisesat least a first fluid delivery outlet 420, through which heated fluidmay be impinged onto first major surface 112 of substrate 110, and asecond fluid delivery outlet 430 through which heated fluid may beimpinged onto first major surface 121 of substrate 120. (Referencesherein to first fluid delivery outlet, second fluid delivery outlet,etc. are used for convenience of differentiating separate outlets, etc.from each other, and should not be interpreted as requiring that thefluids delivered by the different outlets etc. must differ incomposition). First fluid delivery outlet 420 is supplied with heatedfluid by first fluid delivery channel 421 to which it is fluidlyconnected, and second fluid delivery outlet 430 is supplied with heatedfluid by second fluid delivery channel 431 to which it is fluidlyconnected. In some embodiments, nozzle 400 may comprise a singleinterior plenum (chamber) supplied with heated fluid from an externalsource (not shown) by way of supply line 410, with heated fluid beingdirected to first and second fluid delivery outlets 420 and 430 from thesingle common plenum and with first and second fluid delivery outlets420 and 430 thus comprising first and second portions of a singlecontinuous fluid delivery outlet. Thus in such embodiments, first andsecond fluid delivery channels 421 and 431 are portions of a singlecommon plenum rather than being physically separate channels, and firstand second fluid delivery outlet portions 420 and 430 will deliverheated fluid from a common source at similar or identical conditions (insuch case, outlet portions 420 and 430 may simply be differently-facingportions of a single outlet).

In alternative embodiments, the interior of nozzle 400 may be divided(e.g., by optional interior partition 422 of FIG. 9) into first fluiddelivery channel 421 and second fluid delivery channel 431 that arephysically separate and that are not fluidly connected with each other.In such case, second fluid delivery channel 431 and second fluiddelivery outlet 430 may be supplied, by second fluid supply line 411,with a heated fluid that is different (e.g., that is air at a differenttemperature, pressure, velocity, etc.), from the heated fluid suppliedto first fluid delivery channel 421 and first fluid delivery outlet 420.

While the exemplary nozzle 400 of FIGS. 8 and 9 is shown as a singleunit from which heated fluid may be impinged onto first major surface112 of substrate 110 and onto first major surface 121 of substrate 120,it will be appreciated that the herein-discussed impinging may beperformed e.g. by the use of two adjacent but physically separated unitsone of which impinges heated fluid through fluid delivery outlet 420onto first major surface 112 of substrate 110 and the other of whichimpinges heated fluid through fluid delivery outlet 430 onto first majorsurface 121 of substrate 120. Thus, while the term “nozzle” is usedherein for convenience of discussion, the apparatus (e.g., nozzle)described herein should be understood to encompass apparatus in which asingle unit impinges fluid onto both substrates as well as amultiple-unit apparatus in which one unit impinges fluid onto onesubstrate and another unit (which may be a physically separate unit)impinges fluid onto the other substrate.

Typically, nozzle 400 will comprise solid (i.e., impermeable) partitions442 and 442′ that collectively define fluid delivery channels 421 and431. The terminal ends of partitions 442 and 442′ that are closest tosubstrate 110 may collectively define fluid delivery outlet 420 (and maybe the only elements that define fluid delivery outlet 420 if outlet 420does not comprise a fluid-permeable sheet (described later in detail) atits working face. Similarly, the terminal ends of partitions 442 and442′ that are closest to substrate 120 may collectively define fluiddelivery outlet 430.

Partitions 442 and 442′ may be positioned generally parallel to eachother (e.g., in similar manner as shown in FIG. 10 a for partitions 542and 542′, which define fluid delivery channel 521 of nozzle 500 insimilar manner that partitions 442 and 442′ define fluid deliverychannel 421 of nozzle 400), if it is desired that fluid deliverychannels 421 and/or 431 have constant width. Or, the width betweenpartitions 442 and 442′ may vary if it is desired e.g. provide a fluiddelivery channel that narrows or expands as the fluid progresses downthe channel. In addition to partitions 442 and 442′, nozzle 400 maycomprise one or more partitions 415 that define the rear portion ofnozzle 400 (away from the fluid delivery outlets). Thus, nozzle 400 maycomprise at least partitions 442, 442′, and 415, which collectivelyprovide an enclosure into which heated fluid may be supplied by supplyline 410 (and supply line 411, if present), with the primary, or only,pathways for the heated fluid to exit nozzle 400 being through fluiddelivery outlets 420 and 430.

For convenience of description, first fluid delivery outlet 420 ischaracterized as comprising working face 424, which can be mostconveniently considered to be the surface through which the heated fluidpasses as it exits outlet 420. Working face 424 may be an imaginarysurface, such as an imaginary arcuate surface (e.g., a section of acylindrical surface) defined by terminal ends of partitions 442 and442′. Or, working face 424 may comprise a physical layer, e.g. afluid-permeable sheet, as discussed later herein in detail. Second fluiddelivery outlet 430 is likewise characterized as comprising working face434.

Each outlet and working face thereof may have a circumferential length,and a lateral width (extending in a direction transverse to thedirection of motion of the adjacent substrate, i.e. extending in adirection aligned with the long axes of the adjacent backing roll). Insome embodiments, the circumferential length may be longer than thelateral width, so that the outlet is circumferentially elongated. Whilein the exemplary illustration of FIG. 8, first fluid delivery outlet 420extends over the entire circumferential length of the face of nozzle 400that is adjacent to roll 230 (with second fluid delivery outlet 430likewise extending over the entire circumferential length of the face ofnozzle 400 that is adjacent to roll 220), in some embodiments each faceof nozzle 400 can comprise multiple separate fluid delivery outlets.Such multiple outlets may be defined by laterally-oriented dividers andmay be spaced over the circumferential length of a nozzle face, as shownin Example Set 3.

First fluid delivery outlet 420, and second fluid delivery outlet 430,are in diverging relation. The term diverging relation can be defined byway of axis 423 drawn normal to working face 424 of first fluid deliveryoutlet 420, and axis 433 drawn normal to working face 434 of secondfluid delivery outlet 430, as depicted in FIG. 9. By diverging relationis meant that normal axis 423 of first fluid delivery outlet 420, andnormal axis 433 of second fluid delivery outlet 430, when extended fromtheir respective working faces in a direction away from nozzle 400, donot intersect regardless of how far they are extended. By divergingrelation is additionally meant that normal axis 423 and normal axis 433are oriented at least 25 degrees away from each other (by way ofexample, in FIG. 9, normal axis 423 and normal axis 433 are orientedapproximately 90 degrees away from each other). In various embodiments,normal axes 423 and 433 are oriented at least about 40, at least about60, or at least about 80 degrees away from each other. In furtherembodiments, normal axes 423 and 433 are oriented at most about 140, atmost about 120, or at most about 100 degrees away from each other.

Those of ordinary skill in the art will realize that in embodiments witharcuate fluid delivery outlets (described below in more detail), therelative orientation of normal axes 423 and 433 may vary with thecircumferential location along each outlet at which the normal axis ispositioned. In such cases, the denoting that two fluid delivery outletsare in diverging relation means that at least the portions of the twooutlets that are in closest proximity to each other (e.g., the portionsof outlets 420 and 430 that are proximal to salient 435) are indiverging relation. In some cases, e.g. in which at least one of thefluid delivery outlets is circumferentially extended so as to form e.g.a nearly-semicylindrical shape, a portion of that fluid delivery outletthat is distal to the other fluid delivery outlet (e.g., distal tosalient 435) may not be in diverging relation with any or all portionsof the other fluid delivery outlet. Such a case is described laterherein with reference to Examples 1-3. However, in such cases, as longas the above-described condition is met in which at least portions ofthe two outlets that are in closest proximity to each other are indiverging relation, the fluid delivery outlets are still considered tobe in diverging relation as defined herein.

First and second fluid delivery outlets 420 and 430 arranged indiverging relation as disclosed herein may be particularly advantageousfor the directing of heated fluid onto two converging substrates. Inparticular, such fluid delivery outlets in diverging relation allownozzle 400 to be placed closely adjacent to a lamination nip establishedby backing rolls, e.g., in the manner depicted in FIGS. 8 and 9.Although discussed herein primarily in the context of bonding substratestogether, it will be appreciated that the use of fluid delivery outletsarranged in diverging relation may find other uses in the heating ofsubstrates for other purposes.

In the exemplary illustration of FIGS. 8 and 9, first fluid deliveryoutlet 420 is arcuate with working face 424 that is generally congruentwith (that is, has a generally similar shape to and generally parallels)the adjacent surface of backing roll 230. This may be advantageous inallowing working face 424 of first fluid delivery outlet 420 to beplaced in close proximity to backing roll 230. Thus, in variousembodiments, in operation of nozzle 400, working face 424 of first fluiddelivery outlet 420 may be less than about 10, 5 or 2 mm from firstmajor surface 112 of substrate 110, at the point of closest approach.Likewise, in the exemplary illustration of FIGS. 8 and 9, second fluiddelivery outlet 430 is arcuate with a working face 434 that is generallycongruent with the adjacent surface of backing roll 220. This may beadvantageous in allowing working face 434 of second fluid deliveryoutlet 430 to be placed in close proximity to backing roll 220. Invarious embodiments, in operation of nozzle 400, working face 434 ofsecond fluid delivery outlet 430 may be less than about 10, 5 or 2 mmfrom first major surface 121 of substrate 120, at the point of closestapproach.

In particular embodiments, first fluid delivery outlet 420 is arcuatewith a working face 424 that is generally congruent with the adjacentsurface of backing roll 230, and second fluid delivery outlet 430 isarcuate with a working face 434 that is generally congruent with theadjacent surface of backing roll 220. This may allow nozzle 400 to bepositioned such that each working face of each fluid delivery outlet isvery close to the first major surface of its respective substrates.

In embodiments in which outlets 420 and 430 are desired to be closelymated to the adjacent surface of (cylindrical) backing rolls, theworking face of each outlet may comprise an arcuate shape that is asection of a generally cylindrical surface with a radius of curvaturematching that of the surface of the backing roll to which the outlet isto be mated. In situations in which backing roll 220 and backing roll230 are the same diameter, the two fluid delivery outlets thus may besymmetric with the same radius of curvature. However, if backing roll220 and backing roll 230 differ in diameter, as in the embodiment shownin FIGS. 8 and 9, the curvature of first fluid delivery outlet 420 maydiffer from that of second fluid delivery outlet 430.

The circumferential length of each arcuate outlet may differ as desired.For example, in FIGS. 8 and 9, the circumferential length of outlet 420is longer than that of outlet 430. Optionally, one or both outlets maycomprise an adjustable shutter (not shown in any figure) that may beadjusted so as to change the circumferential length of the outlet. Sucha shutter may be used to adjust the dwell time of a substrate in theimpinging heated fluid, e.g. independently of the speed of movement ofthe substrate. In operation of apparatus 1, the position of the shutter,as well as other process variables such as fluid temperature, fluidflowrate, backing roll temperatures, etc., may be manipulated asdesired, e.g. in view of the line speed, thickness and other propertiesof the particular substrates being processed.

Fluid delivery outlet 420 and fluid delivery outlet 430 may be chosen tohave any suitable lateral width. As used herein, lateral means in thedirection transverse to the direction of motion of a substrate to beheated and in a direction parallel to the long axis of the backing roll(i.e., the direction in and out of plane in FIGS. 8 and 9). In someembodiments, particularly those in which at least one of the substratesto be bonded is in the form of a narrow strip (e.g., as in the exemplaryembodiment of FIG. 7), it may be desired that the lateral width of thefluid delivery outlet be relatively narrow (e.g., chosen inconsideration of the width of the substrate to be bonded). In such caseit may further be desired that the fluid delivery outlet be elongated(e.g., circumferentially elongated) in a direction substantially alignedwith the long axis of, and the direction of motion of, the substrate tobe bonded (keeping in mind that the long axis and the direction ofmotion of the substrate may be arcuate when the moving substrate issupported by a backing roll). For example, in FIG. 9, working face 424of outlet 420 is circumferentially elongated along an axis that issubstantially aligned with the long axis and direction of motion ofsubstrate 110.

A circumferential end of first fluid delivery outlet 420, and acircumferential end of second fluid delivery outlet 430, may bepositioned adjacent to each other so as to form protruding salient 435,as shown in exemplary manner in FIG. 9. The angle of approach of the twooutlets to each other may be such that the salient 435 takes the form ofa relatively sharp protrusion, with working face 424 of outlet 420, andworking face 434 of outlet 430, being at an acute angle relative to eachother at their point of closest approach or contact. Such a sharplyprotruding design may advantageously permit salient 435 to be positioneddeep into the converging nip region between backing rolls 220 and 230and may allow heated fluid to be impinged upon substrates substantiallyuntil the instant that the substrates contact each other. In variousembodiments, at their point of closest approach working face 424 ofoutlet 420 and working face 434 of outlet 430 may be at an anglerelative to each other of less than about 70, less than about 50, orless than about 30 degrees.

In some embodiments, the working surface of a fluid delivery outlet maynot be congruent with the backing roll to which it is mated. Forexample, either or both of outlets 420 and 430 could be generally planar(flat) rather than arcuate as shown in FIGS. 8 and 9. While this maymean that the fluid delivery outlet may not be able to be positioned asclose to the backing roll, and the distance from the working face to thebacking roll may vary along the length of the fluid delivery outlet,this may still be acceptable in some cases.

As mentioned, the working face of a fluid delivery outlet may be open;or, it may comprise a fluid-permeable sheet through which the heatedfluid may be passed. Such a fluid-permeable sheet may render the flow ofheated fluid through the outlet more uniform, e.g. over thecircumferential length of the outlet. Additionally, depending on thecharacteristics of the sheet, the sheet may redirect the fluid somewhataway from its original direction of flow through the fluid deliverychannel. For example, with reference to FIG. 9, heated fluid from supply410 may flow through fluid delivery channel 421 in a direction generallyaligned with the long axis of partition 422, but in passing through afluid-permeable sheet at working face 424 of fluid delivery outlet 420the fluid may be at least somewhat directed to flow in a direction moreclosely aligned with normal axis 423 of the working face 424 (e.g., asshown by the multiple arrows denoting fluid flow in FIG. 9). Such adesign may have advantages in causing the heated fluid to be impinged onsubstrate 110 in a direction closer to normal to the substrate, asopposed to impinging on substrate 110 in a more tangential orientation.Similar considerations apply with regard to the presence of afluid-permeable sheet on working face 434 of outlet 430. Internalbaffles (not shown in any figure) within fluid delivery channels 421and/or 431 may also be used to direct the heated fluid in a desireddirection.

In various embodiments, the fluid-permeable sheet may comprisethrough-openings that collectively provide the sheet with a percent openarea of at least about 20, at least about 30, or at least about 40. Infurther embodiments, the fluid-permeable sheet may comprise a percentopen area of at most about 90, at most about 80, or at most about 70. Inspecific embodiments, the fluid-permeable sheet may comprise aperforated screen with through-holes of a diameter of at least about 0.2mm, at least about 0.4 mm, or at least about 0.6 mm. The fluid-permeablesheet may comprise e.g. a perforated screen with through-holes of adiameter of at most about 4 mm, at most about 2 mm, or at most about 1.4mm. The through-holes may be in the form of elongated, e.g.laterally-elongated, slots, as described later in Example 1. Thecombination of percent open area and through-hole size may be chosen toenhance the uniform heating of the substrate. The screen may becomprised of any material with durability and temperature resistancesufficient for the uses outlined herein. Metal screen, e.g. steel, maybe suitable.

The heated fluid may exit the working face of the fluid delivery outletat any suitable linear velocity. The velocity may be affected and/ordetermined by the volumetric flowrate of heated fluid supplied to nozzle400 by supply line 410 (and supply line 411, if present), by the size ofthe fluid delivery outlets, by the percent open area and/or diameter ofthe through-holes in a fluid-permeable sheet (if present) at the workingface of the outlet, etc. As mentioned, in the case that partition 422 ispresent, during operation of apparatus 1 the linear velocity of heatedfluid exiting nozzle 400 through outlet 430 can be controlledindependently of that exiting through outlet 420. The linear velocitywill generally be in the low subsonic range, e.g., less than Mach 0.5,typically less than Mach 0.2. Often, the linear velocity will be in therange of a few meters per second; e.g., less than 50, less than 25, orless than 15 meters per second. As such the heated fluid impingementapparatus and methods used herein can be distinguished from the use ofe.g. hot air knives, which often rely on a linear velocity approachingor exceeding sonic velocity.

The area of working faces 424 and 434 of outlets 420 and 430,respectively, may be chosen so as to heat an area of desired size, andmay be chosen in consideration of the characteristics of the substratesto be heated (e.g., their width, thickness, density, heat capacity,etc.). Often, outlets with working faces in the range of from about 5 to50 square centimeters may be used. The volumetric flowrate of the heatedfluid, and the temperature of the heated fluid, may be chosen asdesired. For melt-bonding applications, the temperature of the heatedfluid may be chosen to be at least equal to, or somewhat above, thesoftening point or melting point of a component of the substrates.

Any suitable heated gaseous fluid may be used, with ambient air being aconvenient choice. However, dehumidified air, nitrogen, an inert gas, ora gas mixture chosen to have a specific effect (e.g. the promotion ofbondability, hydrophobicity, etc.) may be used as desired. The fluid maybe heated by an external heater (not shown in any figure) prior to beingdelivered to nozzle 400 through supply line 410 (and 411, if present).In addition, or instead, heating elements may be supplied within nozzle400; or additional heating (e.g., resistance heating, infrared heating,etc.) of nozzle 400 may be applied.

While heating of substrates and/or bonding of substrates as describedherein may be performed without any special handling of the fluid afterit has been impinged on the substrates (as evidenced by Example Set 3),in certain embodiments it may be advantageous to provide for localremoval of the impinged fluid. By local removal is meant that fluid thathas been impinged on the surface of a substrate by a nozzle is activelyremoved from the local vicinity of the fluid impingement nozzle. This isto be contrasted with processes in which the impinged fluid is passivelyallowed to escape from the local vicinity of the nozzle, either todissipate into the surrounding atmosphere or to be removed by a device(e.g., a hood, shroud, duct, etc.) that is positioned some distance(e.g., at least a decimeter) away from the fluid impingement nozzle.Such local removal can be achieved by the use of a nozzle of the generaltype described earlier herein, comprising a fluid delivery channel witha fluid delivery outlet, with the addition of at least one fluid captureinlet that is locally positioned relative to the fluid delivery outlet.By locally positioned it is meant that at their point of closestapproach to each other, the fluid capture inlet is located less than 10mm from the fluid delivery outlet. In various embodiments, at theirpoint of closest approach, the fluid capture inlet is located less thanabout 5 mm, or less than about 2 mm, from the fluid delivery outlet. Thefluid capture inlet is fluidly connected to a fluid removal channel,through which fluid that has been captured by the fluid capture inletcan be actively removed (e.g., by way of an exhaust line fluidlyconnected to an external suction blower, not shown in any figure). Thefluid capture inlet can locally remove a substantial volume percent ofthe impinged fluid from the local vicinity of the nozzle before theimpinged fluid is able to exit the local vicinity of the substrate andirreversibly disperse into the surrounding atmosphere so as to no longerbe locally removable. In various embodiments, at least about 60%, atleast about 80%, or substantially all, of the volumetric flow of theimpinged fluid is locally removed by the apparatus and methods disclosedherein.

Nozzle 500 with a locally positioned fluid capture inlet is shown inrepresentative manner in FIG. 10 a, which is a partial cross sectionalview along the machine direction of substrate 100 as it passes adjacentto nozzle 500 (with the direction of movement of substrate 100 being outof plane). For simplicity of description, FIG. 10 a only shows a singlefluid delivery channel 521, single fluid delivery outlet 520, and singlesubstrate 100 (in contact with backing surface 201, e.g. of backing roll200), but it should be understood that when used to impinge heated fluidonto two converging substrates in similar manner as described for nozzle400, nozzle 500 will comprise two fluid delivery channels, two fluiddelivery outlets, etc., as will be discussed in further detail withrespect to FIG. 11.

While in the exemplary embodiment of FIG. 10 a, fluid delivery outlet520 and fluid delivery channel 521 thereof, and fluid capture inlets540/540′ and fluid removal channels 541/541′ thereof, are shown as oneunit, with common partitions 542 and 542′ therebetween, it should beunderstood that the herein-discussed impinging and removal of fluids maybe performed by the use of two or more adjacent but physically separatedunits, at least one of which impinges heated fluid through fluiddelivery outlet 520 and at least another of which locally captures theimpinged fluid through fluid capture inlet 540 or 540′. Thus, while theterm “nozzle” is used herein for convenience of discussion, theapparatus (e.g., nozzle) described herein should be understood toencompass apparatus in which a single unit both impinges fluid andcaptures the impinged fluid, as well as multiple-unit apparatus in whichone or more units impinge fluid and one or more additional units (whichmay be physically separate units) capture the impinged fluid.

In similar manner to nozzle 400, nozzle 500 comprises fluid deliveryoutlet 520 comprising working face 524 (which in this case comprisesperforated screen 525), with fluid delivery outlet 520 being fluidlyconnected to fluid delivery channel 521 (of which only the portionproximate to fluid delivery outlet 520 is shown in FIG. 10 a).Additionally, nozzle 500 comprises fluid capture inlets 540 and 540′,each of which is locally positioned relative to fluid delivery outlet520. Fluid capture inlets 540 and 540′ are fluidly connected to fluidremoval channels 541 and 541′, respectively. In the exemplaryconfiguration shown, fluid capture inlets 540 and 540′ laterally flank(that is, they are located on either side of, in a direction transverseto the direction of motion of substrate 100, e.g. in a direction alongthe long axis of backing roll 200) fluid delivery outlet 520. Similarly,fluid removal channels 541 and 541′ laterally flank fluid deliverychannel 521, being separated therefrom only by (solid) partitions 542and 542′, respectively. Fluid removal channel 541 is thus defined on onelateral side by partition 542, and on the other lateral side bypartition 543 (which in this embodiment comprises the external housingof nozzle 500 in this area). Fluid removal channel 541′ is likewisedefined by partitions 542′ and 543′.

Referring again to the simplified one delivery outlet, one-substrateillustration of FIG. 10 a, when active suction is applied to fluidremoval channels 541 and 541′ (e.g., by an external suction fan orblower), a substantial volume percent of the heated fluid that exitsworking face 524 of fluid delivery outlet 520 and is impinged upon firstmajor surface 101 of substrate 100, may be locally captured by fluidcapture inlets 540 and 540′ and removed by way of fluid removal channels541 and 541′. It has been found that such local capture of impingedfluid may alter the flow patterns of the fluid after, during, orpossibly even before it impinges on surface 101 of substrate 100. Forexample, such local capture may modify, reduce or substantiallyeliminate fluid flow stagnation phenomena in which the fluid impingesonto the substrate in such manner as to drastically slow or even stopthe flow of the fluid in certain locations. In altering the flowpatterns, the local capture may advantageously modify (e.g., increase)the heat transfer coefficient between the impinging fluid and thesubstrate in certain locations and/or it may provide a more uniformtransfer of heat across a wider area of the substrate. As evidenced byExamples 1-2, local capture of impinged fluid may furthermore allowheated fluid of lower, e.g. considerably lower, temperature to be usedwhile still heating the substrates sufficiently to allow bonding, incomparison to the impinging fluid temperature needed in the absence ofsuch local capture. Such local capture may also allow faster line speedof substrates to be used.

Working faces 544 and 544′ of fluid capture inlets 540 may be positionedapproximately even with working face 524 of fluid delivery outlet 520,so that working faces 544, 544′ and 524 are generally equidistant fromsurface 101 of substrate 100, as represented by distance 545 in FIG. 10a (in the design of FIG. 10 a, working faces 544 and 544′ of fluidcapture inlets 540 and 540′ comprise imaginary surfaces rather thanfluid-permeable screens). Nozzle 500 may be positioned such that workingface 524 of fluid delivery outlet 520, and working faces 544 and 544′ offluid capture inlets 540, are positioned within about 10, about 5, orabout 2 mm, of first major surface 101 of substrate 100. Terminal ends(closest to substrate 110) of partitions 542 and 543 may be generallyequidistant from substrate 100, as shown in FIG. 10 a. Or, the terminalend of outwardly-flanking partition 543 may be extended closer tosubstrate 110, which may enhance the capturing of impinged fluid byfluid capture inlet 540 (similar considerations apply for fluid captureinlet 540′).

FIGS. 10 a, 10 b and 10 c illustrate embodiments in which working faces544 and 544′ of fluid capture inlets 540 and 540′ are open and do notcomprise a perforated screen or any other type of fluid-permeable sheet.In such instances, the working face of a fluid capture inlet may bedefined primarily by the terminal ends of partitions. For example,working face 544 may be defined at least in part with by terminal endsof partitions 543 and 542, e.g. in combination with terminal ends oflaterally extending partitions not shown in FIG. 10, such as housing 415shown in FIG. 9) However, in various embodiments, a fluid-permeablesheet may be provided at the working face of one or more fluid captureinlets. Such a fluid-permeable sheet may comprise similar properties(e.g., of percent open area etc.) as that of a fluid-permeable sheetprovided at the working face of the fluid delivery inlet to which thefluid capture outlet is locally positioned, and may be a continuation ofthe fluid-permeable sheet of the fluid delivery inlet (e.g., as inExample 1).

In other embodiments, the fluid-permeable sheet of the fluid captureinlet may comprise different properties, and/or be comprised ofdifferent materials, than the fluid-permeable sheet of the fluiddelivery inlet.

FIG. 10 a illustrates an embodiment in which the configuration of nozzle500, the distance from nozzle 500 to substrate 100, the velocity ofimpinging fluid used, etc., combine to provide that substantially all ofthe fluid that exits outlet 520 and impinges on substrate 100 iscaptured by inlets 540 and 540′ before the impinged fluid is able topenetrate laterally beyond the boundaries of inlets 540 and 540′ to anysignificant extent. This phenomenon is represented by the arrowsdenoting direction of fluid flow in FIG. 10 a. (Of course, some smallportion of the fluid that exits outlet 520 may be removed by inlets 540or 540′ before impinging onto substrate 100). FIG. 10 b illustrates anembodiment in which nozzle 500 is operated such that some portion of theimpinged fluid is able to penetrate laterally beyond the boundaries ofinlets 540 and 540′ (and hence may locally mix with ambient air to atleast a small extent) but in which the suction provided by captureinlets 540 and 540′ is sufficiently strong that substantially all of theimpinged fluid is still captured by capture inlets 540 and 540′. FIG. 10c illustrates an embodiment in which nozzle 500 is operated such thatsubstantially all of the impinged fluid is captured by capture inlets540 and 540′, and in which some portion of the ambient air is alsocaptured by the capture inlets (flow of ambient air in FIG. 10 c isindicated by the dashed arrows). When nozzle 500 is operated in thismanner, in various embodiments the volumetric flow rate of capturedambient air can range up to about 10%, up to about 20%, or up to about40%, of the volumetric flow rate of captured impinged fluid.

Those of ordinary skill in the art will appreciate that by the methodsdisclosed herein, impinged fluid may be circulated at least slightlylaterally beyond the boundaries of the fluid capture inlets and yetstill locally captured by the fluid capture inlets and removed. It hasbeen found that adjustment of the design of nozzle 500 and of theoperating parameters of the system (e.g., flowrate of heated fluid,suction applied through the fluid removal channels, etc.) can alter theextent to which the impinged heated fluid is able to penetrate laterallybeyond the boundaries of the fluid capture inlets before being capturedby the capture inlets, and/or can alter the extent to which ambient airis captured in addition to the impinged fluid, either of both of whichcan advantageously enhance the uniformity of the heating experienced bysubstrate 100.

In reviewing FIGS. 10 a, 10 b, and 10 c, those of ordinary skill in theart may realize that in these exemplary illustrations, fluid deliveryoutlet 520 is only bordered by fluid capture inlets 540 and 540′laterally, there being no provision for fluid capture inlets surroundingfluid delivery outlet 520 in the direction of motion of substrate 100 soas to completely surround the perimeter of fluid delivery outlet 520.However, in similar manner as discussed with respect to nozzle 400, andas discussed later with respect to FIG. 11, the inlets and outlets ofnozzle 500 may comprise circumferentially elongated arcuate shapes withthe elongated axis of the inlets and outlets aligned in the direction ofmotion of substrate 100. Thus, in various embodiments, the providing offluid capture inlets 540 and 540′ that laterally flank fluid deliveryoutlet 520 may be sufficient to surround at least about 70%, at leastabout 80%, or at least about 90%, of the perimeter of fluid deliveryoutlet 520 with fluid capture inlets. (Those of skill in the art willalso appreciate that in using nozzle 500 to bond two substrates asdescribed in further detail in reference to FIG. 11, two fluid deliveryoutlets, each laterally flanked by fluid capture inlets, may bepositioned with their circumferential terminal ends in close proximity,which, for the combined outlets, will further minimize the outlet areathat is not bordered by a fluid capture inlet).

While FIGS. 10 a, 10 b, and 10 c only show a single fluid capture inletand a single substrate for convenience of describing the basic premiseof local fluid capture, it will be understood that nozzle 500 may beused to impinge heated fluid on two converging substrates and to locallyremove the impinged fluid from the local vicinity of the nozzle. Such anembodiment is depicted in exemplary manner in FIG. 11. In theillustrated embodiment, nozzle 500 comprises first fluid delivery outlet520 with working face 524, outlet 520 being fluidly connected to firstfluid delivery channel 521, and being laterally flanked by first fluidcapture inlets 540 and 540′ which are fluidly connected to first fluidremoval channels 541 and 541′ (all as described with respect to FIG. 10a). Nozzle 500 additionally comprises second fluid delivery outlet 550with working face 554, outlet 550 being fluidly connected to secondfluid delivery channel 551, and being laterally flanked by second fluidcapture inlets 560 and 560′ with working faces 564 and 564′ respectivelyand which are fluidly connected to second fluid removal channels 561 and561′ respectively. All of these features are analogous to nozzle 400 ofFIG. 9, with the addition of the fluid capture inlets and the fluidremoval channels. As such, fluid delivery channels 521 and 551 may beregarded as substantially equivalent to fluid delivery channels 421 and431 of nozzle 400, and fluid delivery outlets 520 and 550 can beregarded as substantially equivalent to fluid delivery outlets 420 and430 of nozzle 400. Thus, it will be understood that relevantdescriptions of features of nozzle 400, for example thecircumferentially elongated and/or arcuate nature of the outlets, theirpositioning near the substrate, the arranging of the outlets to form aprotruding salient 535, etc., apply in like manner to the features ofnozzle 500. In particular, fluid delivery outlets 520 and 550 of nozzle500 are in diverging relation in the manner previously described. Inparticular embodiments, fluid capture inlets 540 and 540′ may becongruent with fluid delivery outlet 520, all of which may be congruentwith adjacent surface 201 of backing roll 200 (that is, the arcuateshape of all of these elements may be similar and generally parallel toeach other). Similar considerations apply for fluid capture inlets 560and 560′, and fluid delivery outlet 550, with respect to each other andto surface 206 of backing roll 205.

In FIG. 11, only one heated fluid supply line (510) is shown, and fluiddelivery channels 521 and 551 are shown as comprising portions of asingle plenum with no partition (analogous to partition 422 of nozzle400) therebetween. It will be understood that such a partition could beused if desired, and a heated fluid supply line could be used for fluiddelivery channel 551 that is separate from the heated fluid supply lineused for fluid delivery channel 521 (in like manner to that describedfor nozzle 400).

At least one fluid exhaust line 511 is used to remove the captured fluidfrom the fluid removal channels of nozzle 500. In the illustratedembodiment fluid removal channels 541 and 561 comprise portions of asingle fluid removal channel, there being no dividing partition inbetween. Thus in this embodiment a single fluid exhaust line may be usedto remove captured fluid from channels 541 and 561. If a partition isprovided between fluid removal channels 541 and 561, separate fluidexhaust lines can be provided for each fluid removal channel. Similarconsiderations apply to channels 541′ and 561′.

If desired, separate fluid exhaust lines can be connected to fluidremoval channels 541 and 541′. Alternatively, passages can be providedwithin nozzle 500 (e.g., passing laterally through fluid deliverychannel 521), that interconnect fluid removal channels 541 and 541′, sothat a single fluid exhaust line can be used for both. Similarconsiderations apply to channels 561 and 561′.

Fluid delivery outlet 520 may be used to impinge heated fluid onto majorsurface 101 of substrate 100, while substrate 100 is in contact withbacking surface 201 (e.g., of backing roll 200). Likewise, fluiddelivery outlet 550 may be used to impinge heated fluid onto majorsurface 106 of substrate 105, while substrate 105 is in contact withbacking surface 206 (e.g., of backing roll 205). These operations may beconducted in similar manner as described for nozzle 400, except thatfluid capture inlets 540, 540′, and 560 and 560′ are used as describedabove, to locally capture the impinged fluid.

In some cases it may be desirable to provide multiple, laterally spacedfluid delivery outlets each fluidly connected to a fluid deliverychannel. As elsewhere herein, laterally signifies a direction transverseto the direction of motion of the substrate to be heated, e.g. along thelong axis of a backing roll. FIG. 12 shows such an exemplaryconfiguration, again in the simplified context of a single substrate 100with the direction of substrate motion being out of plane of FIG. 12.Exemplary nozzle 600 comprises first and second laterally spaced fluiddelivery outlets 620 and 620′ with working faces 624 and 624′,respectively, and fluidly connected to fluid delivery channels 621 and621′, respectively. In the illustrated embodiment, working faces 624 and624′ comprise perforated screens 625 and 625′, respectively. Outer fluidremoval outlets 640 and 640′ are provided that laterally outwardly flankfluid delivery outlets 620 and 620′. Also provided is additional, innerfluid capture inlet 670 that is laterally sandwiched in between fluiddelivery outlets 620 and 620′. Fluid capture inlets 640, 640′, and 670comprise working faces 644, 644′, and 674, respectively, and are fluidlyconnected to fluid removal channels 641, 641′ and 671 respectively.Outer fluid removal channels 641 and 641′ are separated from fluiddelivery channels 621 and 621′ by partitions 642 and 642′, respectively.Outer fluid removal channels 641 and 641′ are further defined bypartitions 643 and 643′, respectively, which may comprise part of thehousing of nozzle 600 in these locations Inner fluid removal channel 671is separated from fluid delivery channels 621 and 621′ by partitions 672and 672′, respectively.

The descriptions of the various fluid delivery and removal channels,fluid delivery outlets and fluid capture inlets provided earlier hereinwith regard to nozzles 400 and 500, are applicable to the variouschannels, outlets and inlets of nozzle 600. And, of course, while shown(for convenience of description) in FIG. 12 in respect to a singlesubstrate 100, it should be understood that when used to impinge heatedfluid onto two converging substrates in similar manner as described fornozzle 400 and nozzle 500, nozzle 600 will comprise channels, outlets,inlets, etc., as needed to impinge heated fluid upon the two substrates.In particular, nozzle 600 may comprise two laterally spaced pairs offluid delivery outlets with each outlet of a given pair being indiverging relation, and with the laterally spaced pairs of fluiddelivery outlets being laterally outwardly flanked by pairs of fluidcapture inlets and having an additional pair of fluid capture inletslaterally sandwiched therebetween.

As illustrated in FIG. 12, heated fluid exiting working faces 624 and624′ of fluid delivery outlets 620 and 620′ and impinging on substrate100 is locally captured by fluid capture inlets 640, 640′ and 670. Thoseof ordinary skill in the art will appreciate that the interposition ofinner fluid capture inlet 670 laterally in between fluid deliveryoutlets 620 may reduce or eliminate any stagnation points that otherwisemay result from the colliding of fluid from the two outlets. Designs ofthe type depicted in FIG. 12 may provide enhanced uniformity in theheating of wide-width substrates. Additionally, designs of this type maybe advantageous in the case in which it is desired to heat twosubstrates in parallel strips (e.g., to make laminates of the type shownin FIG. 7). In such case fluid delivery outlet 620 may be centeredgenerally over one substrate strip, and fluid delivery outlet 620′ maybe centered over the other.

The basic design of nozzle 600, in which multiple, laterally spacedfluid delivery outlets are used, in which fluid capture inlets arepositioned outwardly laterally flanking the fluid delivery outlets, andin which an additional fluid capture inlet is positioned laterally inbetween the fluid delivery outlets, can be extended as desired. That is,a nozzle may be produced with any number of fluid delivery outlets (withtheir long axis aligned generally in the direction of motion of theweb), laterally interspersed in an alternating manner with fluid captureinlets. As mentioned previously, multiple, physically separate fluiddelivery outlets and fluid capture inlets can be provided, to a similarend. Any such design may allow wide-width substrates to be heated by themethods disclosed herein.

Those of ordinary skill in the art will appreciate that while theapparatus and methods for local removal of impinged fluid may beparticularly advantageous for applications such as heating of substratesto achieve surface-bonding as described herein, many other uses arepossible.

EXAMPLES Example 1

A spunbond nonwoven web available from First Quality Nonwovens under thetrade designation Spunbond 50 gsm (SSS) was obtained. The web was 50 gsmwith a dot pattern of 15% point bond and a width of 100 mm, and wascomprised of polypropylene. A substrate was obtained from 3M Company,St. Paul, Minn. under the trade designation CS600 (of the general typedescribed in U.S. Pat. No. 6,000,106). The first surface of thesubstrate was generally smooth and the second surface of the substratebore protrusions at a density of approximately 2300 per square inch,(with the protrusions being male fastening elements each with anenlarged, generally disc-shaped head). The thickness of the substratewas approximately 100 microns (not counting the height of theprotrusions) and the height of the protrusions was approximately 380microns. The backing and protrusions were of integral construction andwere both comprised of polypropylene/polyethylene copolymer. Thesubstrate was obtained as elongated strips each of 24 mm width.

A web handling apparatus with lamination nip was setup in similar mannerto that that shown in FIG. 8. Two elongated strip substrates were bondedto the first surface of a single nonwoven web as described herein. Whilefor convenience the following description will occasionally be phrasedin terms of one substrate, it will be understood that two identicalsubstrates were identically handled, traveling in parallel.

In using the apparatus, the substrate was guided onto an 10.2 cm radiuschrome preheat roll (analogous to roll 210 of FIG. 8) with the firstsurface of the substrate (that is, the surface opposite the surfacebearing the protrusions) contacting the surface of the preheat roll. Thepreheat roll was internally heated by hot oil to comprise a nominalsurface temperature of approximately 118 degrees C. Upon attainment ofsteady state operating conditions, the first surface of the substratewas found to attain a temperature of approximately 113 degrees C. (asmonitored by a non-contact thermal measurement device).

From the preheat roll the substrate traversed a distance ofapproximately 5.1 cm to a first backing roll (analogous to roll 220 ofFIG. 8) of 3.2 cm radius, which was not actively cooled or heated. Onits surface the roll comprised a nominal 0.64 cm thick surface layer ofsilicone rubber impregnated with aluminum particles. The surface layercomprised a Shore A hardness of 60. The surface layer comprised twoelevated plateaus that circumferentially extended completely around theroll (the plateaus were elevated approximately 2.2 mm above thesurrounding surface of the roll), each of lateral width approximately 27mm, with the lateral distance (across the face of the roll, in adirection aligned with the long axis of the roll) between their nearedges of approximately 8 mm. The parallel-traveling substrates wereguided onto the plateaus of the first backing roll so that themushroom-shaped heads of the protrusions on the second surface of thesubstrate contacted the plateau surface. (The substrates were elevatedon plateaus to minimize the chances of the nonwoven web contacting thesurface the first backing roll.) After thus contacting the surface ofthe first backing roll, the substrates circumferentially traversed anarc of approximately 180 degrees around the first backing roll to beheated and bonded as described herein.

In using the apparatus, the nonwoven web was guided onto a secondbacking roll, of 10.2 cm radius (analogous to roll 230 of FIG. 8). Thesecond backing roll comprised a metal surface and was controlled byinternal circulation of fluid to a nominal temperature of 38 degrees C.The nonwoven web circumferentially traversed an arc of approximately 90degrees around the second backing roll to be heated and bonded asdescribed herein. The path of the nonwoven web was aligned with thepaths of the two substrate strips so that when the two substratescontacted the nonwoven web in the nip between the two backing rolls, thesubstrate strips were aligned downweb with the nonwoven web.

The backing rolls were positioned in a horizontal stack, similar to thearrangement shown in FIG. 8. A heated-air impingement nozzle capable oflocal capture/removal of impinged air, was built and was placedvertically above the backing roll stack, adjacent the nip, in analogousmanner to the placement of nozzle 400 in FIG. 8. As viewed from the sidealong an axis transverse to the web movement (i.e., as viewed in FIG.8), the nozzle comprised a first surface and a second surface, with thefirst and second surfaces being in diverging relation (as definedearlier herein). Each surface comprised a generally cylindrical section,with the curvature of the first surface generally matching the curvatureof the first backing roll (with the radius of curvature of the firstsurface being approximately 3.2 cm) and the curvature of the secondsurface generally matching the curvature of the second backing roll(with the radius of curvature of the second surface being approximately10.2 cm). The circumferential length of the first surface wasapproximately 75 mm and the circumferential length of the second surfacewas approximately 50 mm. The two surfaces met at a protruding salientanalogous to salient 435 of FIG. 9.

As viewed from a direction aligned with the movement of the twosubstrate strips, the first diverging surface of the nozzle comprisedtwo air delivery outlets, each of lateral width approximately 25 mm. Thetwo air delivery outlets were laterally outwardly flanked by two aircapture inlets, each of lateral width approximately 21 mm. Sandwichedlaterally in between the two air delivery outlets was an additional aircapture inlet, of lateral width approximately 4 mm. A perforated metalscreen comprising elongated slot openings was positioned so as to extendtransversely along the first diverging surface so as to cover the twoair-delivery outlets and the air capture inlet therebetween, but notcovering the two outwardly laterally flanking air capture inlets. Theslot openings were elongated in the lateral direction, wereapproximately 0.9 mm in width, and were circumferentially spaced at acenter-to-center spacing of approximately 3.0 mm. The perforated metalscreen comprised a percent open area of approximately 28%. Thus, thefirst surface of the nozzle comprised a configuration analogous to thatshown in FIG. 12, except that the perforated metal screen defined thesandwiched air-capture inlet in addition to defining the workingsurfaces of the air delivery outlets.

When viewed from a direction aligned with the movement of the nonwovenweb, the second diverging surface of the nozzle comprised a similararrangement of two air delivery outlets, two laterally flanking aircapture inlets, and one laterally sandwiched air capture inlet. Thelateral widths of the outlets and inlets were the same as for the firstdiverging surface. The second diverging surface comprised an adjustableshutter that laterally extended so as to laterally cover the width ofboth air delivery outlets and that could be moved circumferentiallyalong the second surface so as to control the circumferential length ofthe air delivery outlets. The shutter was positioned so that thecircumferential length of the air delivery outlets of the seconddiverging surface was approximately 40 mm. The above-describedperforated metal screen covered the two air-delivery outlets and the aircapture inlet therebetween of the second diverging surface, in similarmanner as for the first diverging surface.

All of the air delivery outlets and inlets of the first and seconddiverging surfaces were fluidly connected to air delivery channels andair removal channels, respectively. The air delivery outlets were allfed by the same air delivery conduit attached to the nozzle, so that thesubstrates, and the nonwoven web, received air at generally similartemperatures. The temperature and volumetric flowrate of the heated airsupplied to the nozzle could be controlled as desired (by use of aheater available from Leister, of Kaegiswil, Switzerland, under thetrade designation Lufterhitzer 5000). The volumetric rate of removal ofcaptured air (through a removal conduit attached to the nozzle) could becontrolled as desired.

The nozzle was positioned close to the first and second backing rolls ina manner analogous to the position of nozzle 400 in FIG. 9. The firstdiverging surface of the nozzle was at a distance estimated to beapproximately 1.5 to 2 mm from the surface of the first backing roll,over an arc extending approximately 128 degrees circumferentially aroundfirst backing roll. The second diverging surface of the nozzle was at adistance estimated to be approximately 1.5 to 2 mm from the surface ofthe second backing roll, over an arc extending approximately 28 degreescircumferentially around the second backing roll. The protruding salientwas centered over the nip (the closest point of contact between thesurfaces of the two rolls), again analogous to the configuration shownin FIG. 9.

The heated air supply temperature was measured at 390° F. (198° C.), byuse of several thermocouples and associated hardware. The volumetricflow rate of heated air and captured air was determined using a hot wireanemometer and associated hardware. The volumetric flow of heated airwas approximately 1.0 cubic meters per minute. With the total area ofthe air delivery outlets being approximately 54 cm², and with theperforated metal screen comprising a percent open area of approximately28, the linear velocity of the heated air at the working face of theoutlets was estimated to be approximately 11 meters per second. Thereturn supply volume was approximately 1.14 cubic meters per minute,thus corresponding to capture of ambient air at a volumetric flowrate ofapproximately 14% of that of the captured impinged air.

The above-described apparatus and methods were used to guide theelongated strip substrates and the nonwoven web in an arcuate path alongthe surface of the first and second backing rolls respectively, duringwhich they passed closely by the first and second diverging surfaces(respectively) of the nozzle, to be impinged with heated air with localcapture of impinged air. The substrates and the nonwoven web thenentered the nip between the two backing rolls wherein the first surfacesof the substrates and the first surface of the backing were brought intocontact. The nip between the two backing rolls was set at low pressure,with the pressure estimated to be 5 pli (pounds per linear inch), orapproximately 9 N per linear cm. The line speed of the two substratesand of the nonwoven web was set to nominal 70 meters per minute.

After being contacted together, the substrates and the nonwoven webtogether circumferentially followed the surface of the second backingroll over an arc of approximately 180 degrees before being removed fromcontact with the backing roll.

This process resulted in the bonding of two parallel strips of thesubstrate to the first surface of the nonwoven web, with a strip of thefirst surface of the nonwoven web being exposed between the near edgesof the substrate strips, and with strips of the first surface of thenonwoven web exposed beyond the far edges of the strips (analogous tothe arrangement shown in FIG. 7).

Upon inspection, it was found that the bond between the substrate stripsand the nonwoven web was excellent, and that it was difficult toimpossible to remove the substrate from the nonwoven web withoutsignificantly damaging or destroying one or both. Notably, the bondedarea extended completely over the area of contact between the substrateand the nonwoven web, including the very edges of the substrate. It wasalso noted that the second surface of the nonwoven web (the surfaceopposite the surface to which the substrate was bonded) in areas wherethe substrate was bonded did not differ significantly from areas withoutthe substrate. That is, it did not appear that the bonding processsignificantly altered the loft, density, or appearance of the nonwovenweb. It was also noted that the bonding process did not appear to affector alter the protruding male fastening elements. That is, no physicaldamage or deformation of the elements was noted. Qualitatively, nodifference was observed in the loft of the fibrous web as a result ofhaving undergone the bonding process. Qualitatively, no difference wasobserved in engagement performance of the fastening elements withfibrous materials as a result of having undergone the bonding process.Upon close inspection, the nonwoven web and the substrate were observedto be surface-bonded together, as described herein.

Example 2

A composite nonwoven web was obtained from 3M under the tradedesignation EBL Bright (of the general type described in U.S. Pat. No.5,616,394), which comprised approximately 35 gsm of propylene fiber (4denier) bonded in arcuately protruding loops to a 35 gsm polypropylenebacking. Strips of the substrate material of Example 1 were bonded tothe fiber side of the nonwoven web, using conditions substantially thesame as for Example 1. Excellent results were again found, withexcellent surface-bonding over the entirety of the nonwovenweb-substrate contact area, and without apparent damage or densificationof the nonwoven web and without apparent damage or deformation to themale fastening elements.

Example Set 3

A 50 gsm spunbond-meltblown-spunbond (SMS) nonwoven web was obtainedfrom PGI Nonwovens, Charlotte, N.C., under the trade designationLC060ARWM. Various web widths were used, generally in the range of 10cm. A substrate was obtained from 3M Company, St. Paul, Minn. asdescribed in Example 1. The substrate was obtained as an elongated stripof 20 mm width.

A web handling apparatus with lamination nip was set up. The apparatushad a first backing roll made of metal and a second backing roll made ofwood, with the surface of the wood roll covered by silicone tape(obtained from Tesa, Hamburg Germany, under the trade designation04863). The backing rolls were positioned in a vertical stack with thewood roll atop the metal roll, defining a nip therebetween. Thetemperature of the backing rolls was not controlled. The nonwoven webwas guided over the first, metal backing roll and the substrate wasguided over the second, silicone-covered wood backing roll, with theprotrusions facing toward the backing roll. Idler rollers were placednear the backing rolls to guide the substrate and the nonwoven web sothat each traversed an arc of approximately 130 degrees around itsrespective backing roll.

Heated air was provided by a heater available from Leister, ofKaegiswil, Switzerland, under the trade designation LHS System 60L. Theheated air was impinged onto the substrates by a custom-made nozzle. Thenozzle was made of metal and had a supply inlet (opening) at the rear ofthe nozzle that could be coupled to a heated-air supply conduit. Thebody of the nozzle was made of two laterally-spaced, generally parallel,sidewalls that extended horizontally along the long axis of the nozzlefrom the supply inlet at the rear of the nozzle to a tip at the front ofthe nozzle (closest to the nip). The sidewalls were substantiallyidentical in shape; each had upper and lower edges with a sidewallheight defined therebetween at any given location along the long axis ofthe nozzle. Over the distance from the rear of the nozzle to a locationapproximately halfway between the front and rear of the nozzle, theupper and lower edges of each sidewall diverged so that the sidewallheight increased to a maximum. Over the distance from this location (ofmaximum sidewall height) to the front of the nozzle, the sidewall heightdecreased as the upper and lower edges of the sidewalls each followed asmoothly arcuate, converging path to meet in a point that defined thefront of the nozzle. The arcuate shape of the upper and lower edges ofthe sidewalls were made to generally match the curvature of the woodbacking roll and the metal backing roll, respectively. Thus, the nozzlecomprised an upper front face and a lower front face, the faces indiverging relation to each other, with the front end of the nozzlecomprising a protruding salient.

At the upper and lower front faces of the nozzle, the lateral spacingbetween the sidewalls was approximately 20 mm. The interior of thenozzle was divided by metal partitions so as to provide six rectangularair-delivery outlets each supplied by an air-delivery channel (with allthe channels being supplied with heated air from the same supply inletat the rear of the nozzle). Each air-delivery outlet was approximately20 mm wide laterally, with the vertical height of the outlets rangingfrom approximately 2.5 mm to 4.0 mm (since the nozzle was custom-built,there was some variability in the dimensions). One of the air-deliveryoutlets was at the protruding tip at the front of the nozzle, and wasoriented to deliver heated air generally directly toward the nipestablished by the two backing rolls. The upper face of the nozzle hadthree air-delivery outlets, oriented to deliver heated air to thesubstrate as it traversed an arc of approximately 45 degrees around theupper backing roll immediately prior to passing through the nip. Thelower face of the nozzle had two air-delivery outlets, oriented todeliver heated air onto the nonwoven web as it traversed an arc ofapproximately 45 degrees around the lower backing roll immediately priorto passing through the nip. The air-delivery outlets were open with noperforated metal screen being present. In between the air-deliverychannels within the interior of the nozzle were dead spaces (throughwhich heated air did not pass). Holes were provided in the sidewalls ofthe nozzle in these dead space locations to provide venting. The nozzledid not contain any air capture inlets and no provision was made forlocal removal of impinged air.

In various experiments using the apparatus, the nozzle was positioned sothat the air-delivery outlets of the upper face of the nozzle wereestimated to be in the range of 3-4 mm from the face of the upperbacking roll, and so that the air-delivery outlets of the lower face ofthe nozzle were similarly an estimated 3-4 mm from the face of the lowerbacking roll. In these experiments, heated air was provided at variousvolumetric flowrates. It was not possible to measure the actualvolumetric flowrates during the experiments, but off-line testingindicated that the volumetric flowrates were in the range of severalhundred liters per minute. In these experiments, heated air was providedat various temperatures, ranging from approximately 500 degrees C. toapproximately 700 degrees C. In these experiments, the substrate and thenonwoven web were guided onto their respective backing rolls, passed andfront of the nozzle, and contacted with each other, at various linesspeeds over the range of 105-210 meters per minute. Within these generalconditions, the nonwoven web and the substrate were able to be bondedtogether to provide a surface-bonded laminate as described herein,without apparent damage or densification of the nonwoven web and withoutapparent damage or deformation to the male fastening elements. Withinthese general conditions, it was found that, with the combination ofsubstrates and nozzle used in these experiments, more robust bonding wasachieved at higher temperatures and/or at lower line speeds. However,the degree of bonding that is suitable may vary with the particularapplication for which the laminate is to be used.

The tests and test results described above are intended solely to beillustrative, rather than predictive, and variations in the testingprocedure can be expected to yield different results. All quantitativevalues in the Examples section are understood to be approximate in viewof the commonly known tolerances involved in the procedures used. Theforegoing detailed description and examples have been given for clarityof understanding only. No unnecessary limitations are to be understoodtherefrom.

It will be apparent to those skilled in the art that the specificexemplary structures, features, details, configurations, etc., that aredisclosed herein can be modified and/or combined in numerousembodiments. All such variations and combinations are contemplated bythe inventor as being within the bounds of the conceived invention.Thus, the scope of the present invention should not be limited to thespecific illustrative structures described herein, but rather by thestructures described by the language of the claims, and the equivalentsof those structures. To the extent that there is a conflict ordiscrepancy between this specification and the disclosure in anydocument incorporated by reference herein, this specification willcontrol. This application is related to U.S. Provisional PatentApplication Ser. No. ______ titled BONDED SUBSTRATES AND METHODS FORBONDING SUBSTRATES, Docket No. 65871US002, filed evendate herewith,which is herein incorporated by reference in its entirety.

1. An apparatus for impinging fluid onto at least a first surface of afirst moving substrate and a first surface of a second moving substrateand locally removing the impinged fluid, comprising: at least one firstfluid delivery outlet; at least one first fluid capture inlet that islocally positioned relative to the first fluid delivery outlet; at leastone second fluid delivery outlet; at least one second fluid captureinlet that is locally positioned relative to the second fluid deliveryoutlet; and wherein the at least one first fluid delivery outlet and theat least one second fluid delivery outlet are in diverging relation. 2.The apparatus of claim 1 further comprising at least one first fluiddelivery channel fluidly connected to the at least one first fluiddelivery outlet, at least one second fluid delivery channel fluidlyconnected to the at least one second fluid delivery outlet, at least onefirst fluid removal channel fluidly connected to the at least one firstfluid capture inlet, and at least one second fluid removal channelfluidly connected to the at least one second fluid delivery outletdelivery outlet.
 3. The apparatus of claim 2 wherein the first andsecond fluid delivery channels comprise first and second portions of acommon fluid delivery plenum.
 4. The apparatus of claim 1 wherein thefirst fluid delivery outlet comprises a circumferentially elongatedarcuate shape and wherein the first fluid capture inlet comprises acircumferentially elongated arcuate shape that is congruent with that ofthe first fluid capture inlet; and, wherein the second fluid deliveryoutlet comprises a circumferentially elongated arcuate shape and whereinthe second fluid capture inlet comprises a circumferentially elongatedarcuate shape that is congruent with that of the second fluid captureinlet.
 5. The apparatus of claim 4 wherein the first fluid deliveryoutlet is laterally outwardly flanked by a pair of first fluid captureinlets and wherein the second fluid delivery outlet is laterallyoutwardly flanked by a pair of second fluid capture inlets.
 6. Theapparatus of claim 5 wherein the first fluid capture inlets are bothcongruent with the first fluid delivery outlet, and wherein the secondfluid capture inlets are both congruent with the second fluid deliveryoutlet.
 7. The apparatus of claim 4 wherein a circumferential end of thefirst fluid delivery outlet and a circumferential end of the secondfluid delivery outlet are positioned adjacent to each other so as toform a protruding salient.
 8. The apparatus of claim 4 wherein theapparatus comprises a laterally-spaced pair of first fluid deliveryoutlets, with a pair of first fluid capture inlets laterally outwardlyflanking the pair of first fluid delivery outlets and with an additionalfirst fluid capture inlet laterally sandwiched between the pair of firstfluid delivery outlets; and wherein the apparatus further comprises alaterally-spaced pair of second fluid delivery outlets, with a pair ofsecond fluid capture inlets laterally outwardly flanking the pair ofsecond fluid delivery outlets and with an additional second fluidcapture inlet laterally sandwiched between the pair of second fluiddelivery outlets.
 9. The apparatus of claim 4 wherein the apparatuscomprises at least three laterally-spaced first fluid delivery outlets,with a first fluid capture inlet laterally sandwiched in between eachtwo first fluid delivery outlets, and with a set of first fluid captureinlets laterally outwardly flanking the laterally outwardmost firstfluid delivery outlets; and, wherein the apparatus further comprises atleast three laterally-spaced second fluid delivery outlets, with asecond fluid capture inlet laterally sandwiched in between each twosecond fluid delivery outlets, and with a set of second fluid captureinlets laterally outwardly flanking the laterally outwardmost secondfluid delivery outlets.
 10. The apparatus of claim 5 wherein the fluiddelivery outlets collectively comprise a perimeter and wherein the fluidcapture inlets are positioned and sized so that at least 70% of thecollective outlet perimeter is circumscribed by the fluid captureinlets.
 11. The apparatus of claim 1 wherein each of the fluid deliveryoutlets comprises a working face comprising a fluid-permeable sheet. 12.The apparatus of claim 11 wherein each fluid-permeable sheet comprises adiscontinuous screen with through-openings providing the sheet with apercent open area of between 20% and 80%.
 13. The apparatus of claim 11wherein the fluid-permeable sheet of each fluid delivery outlet ispositioned at an acute angle to the general direction of fluid flow downa fluid delivery channel to which the fluid delivery outlet is fluidlyconnected.
 14. A method of impinging heated fluid onto, and locallyremoving the impinged fluid from, a first surface of a first movingsubstrate and a first surface of a second moving substrate, the methodcomprising: providing at least one first fluid delivery outlet and atleast one first fluid capture inlet that is locally positioned relativeto the first fluid delivery outlet; providing at least one second fluiddelivery outlet and at least one second fluid capture inlet that islocally positioned relative to the second fluid delivery outlet; passingthe first moving substrate by the first fluid delivery outlet andimpinging heated fluid from the first outlet onto the first majorsurface of the first moving substrate; passing the second movingsubstrate by the second fluid delivery outlet and impinging heated fluidfrom the second outlet onto the first major surface of the second movingsubstrate; and, locally capturing at least 60% of the total volumetricflow of impinged fluid by way of the fluid capture inlets and removingthe locally captured fluid through fluid removal channels that arefluidly connected to the fluid capture inlets; and wherein the first andsecond moving substrates are converging substrates.
 15. The method ofclaim 14 comprising locally capturing at least 80% of the volumetricflow of impinged fluid.
 16. The method of claim 14 comprising locallycapturing substantially all of the volumetric flow of impinged fluid.17. The method of claim 16 wherein ambient air from an atmospheresurrounding the moving substrates is captured by the fluid captureinlets and removed by the fluid removal channels, the volumetric flow ofcaptured ambient air being at least about 20% of the volumetric flow ofthe locally captured impinged fluid.
 18. The method of claim 14 whereinthe at least one first fluid delivery outlet and the at least one secondfluid delivery outlet are in diverging relation.
 19. The method of claim14 wherein the at least one first fluid delivery outlet and the at leastone first fluid capture inlet are each positioned less than 5 mm fromthe first surface of the first moving substrate and wherein the at leastone second fluid delivery outlet and the at least one second fluidcapture inlet are positioned less than 5 mm from the first surface ofthe second moving substrate.
 20. The method of claim 14 wherein the atleast one first fluid delivery outlet and the at least one first fluidcapture inlet are each positioned less than 2 mm from the first surfaceof the first moving substrate and wherein the at least one second fluiddelivery outlet and the at least one second fluid capture inlet arepositioned less than 2 mm from the first surface of the second movingsubstrate.
 21. The method of claim 14 wherein the nominal velocity ofthe fluid passing through the outlets is less than 0.2 Mach.
 22. Themethod of claim 14 wherein the first fluid delivery outlet comprises anelongated shape with a long axis, and wherein a pair of first fluidcapture inlets, each with an elongated shape with a long axis, arepositioned in a laterally outwardly flanking relationship with the firstfluid delivery outlet, with the long axis of the first fluid captureinlets being generally parallel to the long axis of the first fluiddelivery outlet, and wherein the long axis of the first fluid captureinlets and of the first fluid delivery outlet are generally aligned withthe direction of motion of the first substrate; and, wherein the secondfluid delivery outlet comprises an elongated shape with a long axis, andwherein a pair of second fluid capture inlets, each with an elongatedshape with a long axis, are positioned in a laterally outwardly flankingrelationship with the second fluid delivery outlet, with the long axisof the second fluid capture inlets being generally parallel to the longaxis of the second fluid delivery outlet, and wherein the long axis ofthe second fluid capture inlets and of the second fluid delivery outletare generally aligned with the direction of motion of the secondsubstrate.
 23. The method of claim 22 wherein the first fluid deliveryoutlet is one of a pair of laterally-spaced first fluid deliveryoutlets, with the pair of first fluid capture inlets laterally outwardlyflanking the pair of first fluid delivery outlets and with an additionalfirst fluid capture inlet laterally sandwiched between the pair of firstfluid delivery outlets; and, wherein the second fluid delivery outlet isone of a pair of laterally-spaced second fluid delivery outlets, withthe pair of second fluid capture inlets laterally outwardly flanking thepair of second fluid delivery outlets and with an additional secondfluid capture inlet laterally sandwiched between the pair of secondfluid delivery outlets.
 24. The method of claim 14 wherein the firstmoving substrate is in contact with the surface of a first backing rolland the second moving substrate is in contact with the surface of asecond backing roll, and wherein the first fluid delivery outletcomprises an arcuate shape generally congruent with the surface of thefirst backing roll, and wherein the second fluid delivery outletcomprises an arcuate shape generally congruent with the surface of thesecond backing roll.
 25. The method of claim 14 further comprisingbringing the first surface of the first moving substrate and the firstsurface of the second moving substrate into contact with each other.